CN213178908U - Rectangular wave fin for ultrathin evaporator core - Google Patents
Rectangular wave fin for ultrathin evaporator core Download PDFInfo
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- CN213178908U CN213178908U CN202021875225.9U CN202021875225U CN213178908U CN 213178908 U CN213178908 U CN 213178908U CN 202021875225 U CN202021875225 U CN 202021875225U CN 213178908 U CN213178908 U CN 213178908U
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Abstract
The utility model discloses a rectangular wave fin for an ultra-thin evaporator core, which comprises a collecting pipe and a core positioned in the center of the collecting pipe; the core body comprises flat pipes and fins arranged on the flat pipes; the thickness X of the core body is 26-33 mm, and the chamfer angle R of the fin is 0.2-0.3 mm; the angle of windowing of fin sets up to 37 ~ 42. The chamfer R of the fin is reduced, and the contact limited length of the fin with the flat pipe at each wavelength is increased. Meanwhile, the reduction of R also enables the windowing length L of the fin to be increased, and the ventilation performance of the fin is improved. On the other hand, the R angle is reduced, the hydrophilic angle of the fin is reduced, and the water-hanging rate of the surface of the fin is reduced. Through to core thickness, windowing number, the comprehensive CFD analysis of windowing angle, design 37 ~ 42 to the windowing angle that thickness is 26 ~ 33mm thickness core, on the contact of shorter wind direction, fully break up the convection current of air side, improve the heat-sinking capability of wind side.
Description
Technical Field
The utility model relates to an air conditioning system technical field, especially a rectangular wave fin for ultra-thin evaporator core.
Background
The structure of a parallel flow type evaporator in the industry at present adopts a double-layer flat tube structure, flat tubes and fins are stacked at intervals, and a manifold is added at two ends of the parallel flow type evaporator to collect and distribute liquid. From the heat transmission aspect, the fin is on guaranteeing to transmit the heat of air side to the refrigerant through flat pipe to form the heat exchange and reach the purpose of cooling in the car.
The main function of the fins is wind side heat dissipation, so that wind resistance can be formed by the fins and air flowing, heat transfer is formed between the fins and the flat tubes, and heat on the air side is brought to a refrigerant in the flat tubes. Therefore, the contact area between the fins and the flat tubes and the heat exchange between the fins and the air side fully determine the heat exchange capability of the fins.
The fin that present evaporimeter core adopted is the rectangular wave fin basically, considers based on core thickness and windage coefficient, and rectangular wave fin windowing angle leads to the fin to windowing inadequately at 33 ~ 36 degrees, and wind side heat transfer ability is not good, and fin and flat pipe area of contact are not big, and heat transfer efficiency is not high, and the evaporimeter core body hangs water easily simultaneously, increases the windage.
SUMMERY OF THE UTILITY MODEL
The utility model discloses an it is not good that aim at overcomes current rectangular wave fin's core wind side heat transfer ability, and the fin is not big with flat tub of area of contact, and heat transfer efficiency is not high, and the evaporator core body hangs water easily simultaneously, increases the windage problem, provides one kind and is used for ultra-thin evaporator core.
A rectangular wave fin for an ultrathin evaporator core comprises a collecting pipe and a core body positioned in the center of the collecting pipe; the core body comprises flat pipes and fins arranged on the flat pipes; the chamfer angle R of the fin is 0.2-0.3 mm; the angle of windowing of fin sets up to 37 ~ 42.
Further, the thickness X of the core body is 26-33 mm.
Further, the collecting pipe is a B-shaped pipe.
Furthermore, a flow passage partition plate is arranged inside the collecting pipe
Furthermore, the flow channel clapboard is profiled on the flow channel section of the collecting pipe.
Furthermore, the windowing length is L, the wave height is H, and the chamfer angle is R, wherein L is less than H-2R-0.2 mm.
The utility model has the advantages that:
1. through the optimal design to the rectangular wave fin, reduce fin chamfer R, increased on every wavelength of fin with flat tub limited length of contact. Meanwhile, the reduction of R also enables the windowing length L of the fin to be increased, and the ventilation performance of the fin is improved. On the other hand, the R angle is reduced, the hydrophilic angle of the fin is reduced, and the water-hanging rate of the surface of the fin is reduced.
2. Through to core thickness, windowing number, the comprehensive CFD analysis of windowing angle, design 37 ~ 42 to the windowing angle that thickness is 26 ~ 33mm thickness core, on the contact of shorter wind direction, fully break up the convection current of air side, improve the heat-sinking capability of wind side.
Drawings
FIG. 1 is a schematic front view of a core;
FIG. 2 is a schematic top view of the core;
FIG. 3 is a partial schematic view of a fin;
FIG. 4 is a schematic view of the windowing angle of the fins;
in the figure, 1-collecting pipe, 2-core, 3-flat pipe, 4-fin and 5-flow channel clapboard.
Detailed Description
The following description of the embodiments of the present invention is provided for illustrative purposes, and other advantages and effects of the present invention will be readily apparent to those skilled in the art from the disclosure herein. The present invention can also be implemented or applied through other different specific embodiments, and various details in the present specification can be modified or changed based on different viewpoints and applications without departing from the spirit of the present invention. It is to be noted that the features in the following embodiments and examples may be combined with each other without conflict.
It should be noted that the drawings provided in the following embodiments are only for illustrating the basic concept of the present invention, and the components related to the present invention are only shown in the drawings rather than drawn according to the number, shape and size of the components in actual implementation, and the form, amount and ratio of the components in actual implementation may be changed at will, and the layout of the components may be more complicated.
Example 1:
as shown in fig. 1 to 4, a rectangular wave fin for an ultrathin evaporator core comprises a collecting pipe 1 and a core 2 located in the center of the collecting pipe 1; the core body 2 comprises flat pipes 3 and fins 4 arranged on the flat pipes 3; the thickness X of the core body 2 is 26-33 mm, and the chamfer angle R of the fin 4 is 0.2-0.3 mm.
The root chamfer angle of the rectangular wave fin is controlled to be 0.2-0.3 mm, and the length L of the contact flat tube is P/2-2Rx2 in the length direction of the fin, namely L is P-4R. P is the wave pitch of the fins, and R is the chamfer angle of the rectangular part of the fins. Meanwhile, the maximum windowing length L of the fin is less than H-2R-0.2 mm. H is the fin wave height.
The thickness of the core 2 is 33 mm. According to the specification of H5-P2.6, the wave height of the fin is 5mm, the wave distance is 2.6mm,
before optimizing the contact length between the fin 4 and the flat tube 3, W is 2.6-4x 0.3-1.4 mm, after optimizing, the contact length W' is 2.6-4x 0.2-1.8 mm, and the effective heat transfer length is increased by 1.8-1.4/1.4x 100-15.8%;
meanwhile, the water hanging rate of the fins is effectively reduced due to the reduction of the R angle of the rectangular fins;
before optimizing the windowing length of the fin, L is less than 5-2 xR-0.2-4.2 mm, and after optimizing, L' is less than 5-2 xR-0.2-4.4 mm; the fin windowing length is increased by 4.4-4.2/4.2x 100% — 4.76%. Through the optimal design to the rectangular wave fin, reduce fin chamfer R, increased on every wavelength of fin with flat tub limited length of contact. Meanwhile, the reduction of R also enables the windowing length L of the fin to be increased, and the ventilation performance of the fin is improved. On the other hand, the R angle is reduced, the hydrophilic angle of the fin is reduced, and the water-hanging rate of the surface of the fin is reduced.
As shown in FIG. 4, the opening angle of the fin 4 is set to be 37-42 degrees. Where K is the fin width. The window opening angle of the core body with the thickness X of 26-33 mm is designed to be 37-42 degrees, the convection of the air side is fully dispersed on the short wind direction contact, and the heat dissipation capacity of the wind side is improved. Although the opening angle of the fins is increased, the wind resistance is not changed actually due to the shortening of the upward distance of the flow direction of the ultrathin core wind, and the requirement of a host factory on the wind resistance of the core in the HVAC can be met. Through to core thickness, windowing number, the comprehensive CFD analysis of windowing angle, design 37 ~ 42 to the windowing angle that thickness is 26 ~ 33mm thickness core, on the contact of shorter wind direction, fully break up the convection current of air side, improve the heat-sinking capability of wind side.
The collecting pipe 1 is a B-shaped pipe. The collecting pipe 1 is also internally provided with a flow passage clapboard 5, and the flow passage clapboard 5 is profiled on the flow passage section of the collecting pipe 1. The uniformity of the refrigerant distributed to the flat pipes 3 can be improved through the runner partition plates 5 arranged in a profiling manner.
Through the optimized evaporator fin, the heat exchange capacity of the core body on the high-efficiency ultrathin evaporator core body is improved to 3-5%, namely the refrigeration capacity of the core body with the original 5KW standard heat exchange capacity can be improved by 150-250W.
The above-mentioned embodiments only express the specific embodiments of the present invention, and the description thereof is specific and detailed, but not construed as limiting the scope of the present invention. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention.
Claims (4)
1. A rectangular wave fin for an ultrathin evaporator core comprises a collecting pipe (1) and a core body (2) positioned in the center of the collecting pipe (1); the core body (2) comprises flat pipes (3) and fins (4) arranged at the flat pipes (3); the method is characterized in that: the chamfer angle R of the fin (4) is 0.2-0.3 mm; the windowing angle of the fin (4) is set to be 37-42 degrees.
2. A rectangular wave fin for an ultra thin evaporator core in accordance with claim 1, wherein: the thickness X of the core body (2) is 26-33 mm, and the width of the corresponding fin is 26-33 mm.
3. A rectangular wave fin for an ultra thin evaporator core in accordance with claim 1, wherein: the collecting pipe (1) is a B-shaped pipe.
4. A rectangular wave fin for an ultra thin evaporator core in accordance with claim 1, wherein: the length of the window is L, the wave height is H, and the chamfer angle is R, wherein L is less than H-2R-0.2 mm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202021875225.9U CN213178908U (en) | 2020-09-01 | 2020-09-01 | Rectangular wave fin for ultrathin evaporator core |
Applications Claiming Priority (1)
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CN202021875225.9U CN213178908U (en) | 2020-09-01 | 2020-09-01 | Rectangular wave fin for ultrathin evaporator core |
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CN213178908U true CN213178908U (en) | 2021-05-11 |
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CN202021875225.9U Active CN213178908U (en) | 2020-09-01 | 2020-09-01 | Rectangular wave fin for ultrathin evaporator core |
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2020
- 2020-09-01 CN CN202021875225.9U patent/CN213178908U/en active Active
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